<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE ep-patent-document PUBLIC "-//EPO//EP PATENT DOCUMENT 1.4//EN" "ep-patent-document-v1-4.dtd"><!-- Disclaimer: This ST.36 XML data has been generated from A2/A1 XML data enriched with the publication date of the A3 document - March 2013 - EPO - Directorate Publication - kbaumeister@epo.org --><ep-patent-document id="EP97116357A3" file="EP97116357NWA3.xml" lang="en" doc-number="0834950" date-publ="19980513" kind="A3" country="EP" status="N" dtd-version="ep-patent-document-v1-4"><SDOBI lang="en"><B000><eptags><B001EP>ATBECHDEDKESFRGBGRITLILUNLSEMCPTIESILTLVFIRO....................................</B001EP><B005EP>R</B005EP><B007EP>DIM360 (Ver 1.5  21 Nov 2005) -  1100000/0</B007EP></eptags></B000><B100><B110>0834950</B110><B120><B121>EUROPEAN PATENT APPLICATION</B121></B120><B130>A3</B130><B140><date>19980513</date></B140><B190>EP</B190></B100><B200><B210>97116357.1</B210><B220><date>19970919</date></B220><B250>en</B250><B251EP>en</B251EP><B260>en</B260></B200><B300><B310>721640  </B310><B320><date>19960926</date></B320><B330><ctry>US</ctry></B330></B300><B400><B405><date>19980513</date><bnum>199820</bnum></B405><B430><date>19980408</date><bnum>199815</bnum></B430></B400><B500><B510><B516>6</B516><B511> 6H 01M   8/24   A</B511><B512> 6H 01M   8/12   B</B512><B512> 6B 01D  53/32   B</B512><B512> 6C 03C  10/00   B</B512><B512> 6C 04B  35/20   B</B512><B512> 6C 04B  35/443  B</B512></B510><B540><B541>de</B541><B542>Flacher Festelektrolyt-Brennstoffzellenstapel mit Polarisationselektroden und versetzten Dichtungen, als Sauerstoffpumpe arbeitend</B542><B541>en</B541><B542>Planar solid electrolyte cell stack working as oxygen pump, with offset seals and biasing electrodes</B542><B541>fr</B541><B542>Batterie de piles à combustible à électrolyte solide, avec garnitures d'étanchéité décalées et électrodes de polarisation, opérant comme pompe à oxygène</B542></B540><B590><B598>7A  7B  </B598></B590></B500><B700><B710><B711><snm>AIR PRODUCTS AND CHEMICALS, INC.</snm><iid>00215775</iid><irf>52 406 V</irf><adr><str>7201 Hamilton Boulevard</str><city>Allentown, PA 18195-1501</city><ctry>US</ctry></adr></B711></B710><B720><B721><snm>Adler, Stuart</snm><adr><str>1723 S. 1800E.</str><city>Salt Lake City, UT 84108</city><ctry>US</ctry></adr></B721><B721><snm>Cutler, Raymond Ashton</snm><adr><str>1574 South 1175 East</str><city>Bountiful,
Utah 84010</city><ctry>US</ctry></adr></B721><B721><snm>Henderson, Brett Tamatea</snm><adr><str>2022 Imperial Street</str><city>Salt Lake City, UT 84105</city><ctry>US</ctry></adr></B721><B721><snm>Ludlow, Jimmy</snm><adr><str>1925 E. 1700S.</str><city>Salt Lake City, UT 84108</city><ctry>US</ctry></adr></B721><B721><snm>Richards, Robin Edward</snm><adr><str>1350 Michael Way</str><city>Lansdale, PA 19446</city><ctry>GB</ctry></adr></B721><B721><snm>Taylor, Dale M.</snm><adr><str>1175 Castlecreek Circle</str><city>Salt Lake City, UT 84117</city><ctry>US</ctry></adr></B721><B721><snm>Wilson, Merrill Anderson</snm><adr><str>3528 West 7260 South</str><city>West Jordan, UT 84084</city><ctry>US</ctry></adr></B721></B720><B740><B741><snm>Schwabe - Sandmair - Marx</snm><iid>00100951</iid><adr><str>Stuntzstrasse 16</str><city>81677 München</city><ctry>DE</ctry></adr></B741></B740></B700><B800><B840><ctry>AT</ctry><ctry>BE</ctry><ctry>CH</ctry><ctry>DE</ctry><ctry>DK</ctry><ctry>ES</ctry><ctry>FI</ctry><ctry>FR</ctry><ctry>GB</ctry><ctry>GR</ctry><ctry>IE</ctry><ctry>IT</ctry><ctry>LI</ctry><ctry>LU</ctry><ctry>MC</ctry><ctry>NL</ctry><ctry>PT</ctry><ctry>SE</ctry></B840><B844EP><B845EP><ctry>AL</ctry></B845EP><B845EP><ctry>LT</ctry></B845EP><B845EP><ctry>LV</ctry></B845EP><B845EP><ctry>RO</ctry></B845EP><B845EP><ctry>SI</ctry></B845EP></B844EP><B880><date>19980513</date><bnum>199820</bnum></B880></B800></SDOBI><abstract id="abst" lang="en"><p id="pa01" num="0001">An electrochemical device for separating oxygen from an oxygen-containing gas comprises a plurality of planar ion-conductive solid electrolyte plates and electrically-conductive gas-impermeable interconnects assembled in a multi-cell stack. Electrically-conductive anode and cathode material is applied to opposite sides of each electrolyte plate. A gas-tight anode seal is bonded between the anode side of each electrolyte plate and the anode side of the adjacent interconnect. A biasing electrode, applied to the anode side of each electrolyte plate between the anode seal and the edge of the anode, eliminates anode seal failure by minimizing the electrical potential across the seal. The seal potential is maintained below about 40 mV and preferably below about 25 mV. A gas-tight seal is applied between the cathode sides of each electrolyte plate and the adjacent interconnect such that the anode and cathode seals are radially offset on opposite sides of the plate. The combination of biasing electrodes and offset seals is particularly effective in eliminating anode seal failure.<img id="iaf01" file="imgaf001.tif" wi="82" he="26" img-content="drawing" img-format="tif" /><img id="iaf02" file="imgaf002.tif" wi="82" he="25" img-content="drawing" img-format="tif" /></p></abstract><search-report-data id="srep" srep-office="EP" date-produced="" lang=""><doc-page id="srep0001" file="srep0001.tif" type="tif" orientation="portrait" he="297" wi="210" /><doc-page id="srep0002" file="srep0002.tif" type="tif" orientation="portrait" he="297" wi="210" /></search-report-data></ep-patent-document>